公开(公告)号：EP3374473B1

公开(公告)日：2024-05-01

申请号：EP16798312.1

申请日：2016-10-24

IPC分类号： C10M101/02 ,  C10M109/02 ,  C10M171/02 ,  C10G50/02 ,  C10G57/00 ,  C10G69/00 ,  C10G69/02 ,  C10G69/12 ,  C10N20/02 ,  C10N20/04 ,  C10N30/02 ,  C10N30/10 ,  C10N40/04 ,  C10N60/02 ,  C10N70/00

CPC分类号： C10G50/02 ,  C10G69/126 ,  C10M171/02 ,  C10M109/02 ,  C10G2300/20220130101 ,  C10G2300/30220130101 ,  C10G2300/30420130101 ,  C10M2203/102520130101 ,  C10M2205/028520130101 ,  C10M2205/17320130101 ,  C10G57/00 ,  C10G69/02 ,  C10M101/02 ,  C10G2400/1020130101 ,  C10M2203/100620130101 ,  C10N2020/0420130101 ,  C10N2020/0220130101 ,  C10N2030/0220130101 ,  C10N2030/1020130101 ,  C10N2040/0420130101 ,  C10N2060/0220130101 ,  C10N2070/0020130101

公开(公告)号：EP3393657A1

公开(公告)日：2018-10-31

申请号：EP16823465.6

申请日：2016-12-20

申请人： Exxonmobil Research And Engineering Company

发明人： PODSIADLO, Paul ,  MCCARTHY, Stephen J. ,  BALIBAN, Richard C. ,  MILLER, Amanda K.

IPC分类号： B01J29/44 ,  B01J29/46 ,  B01J29/48 ,  B01J29/70 ,  B01J37/00 ,  B01J37/02 ,  C10G45/08 ,  C10G45/10 ,  C10G45/12 ,  C10G45/62 ,  C10G45/64 ,  C10G65/04

CPC分类号： C10G69/02 ,  B01J29/44 ,  B01J29/46 ,  B01J29/48 ,  B01J29/703 ,  B01J29/7461 ,  B01J29/7861 ,  B01J37/0009 ,  B01J37/0018 ,  B01J37/0203 ,  B01J2229/186 ,  B01J2229/42 ,  C10G45/08 ,  C10G45/10 ,  C10G45/12 ,  C10G45/62 ,  C10G45/64 ,  C10G65/043 ,  C10G2300/202 ,  C10G2300/70 ,  C10G2400/04 ,  C10G2400/10

摘要： Methods and catalysts are provided for performing dewaxing of diesel boiling range fractions, such as trim dewaxing, that allow for production of diesel boiling range fuels with improved cold flow properties at desirable yields. In some aspects, the methods can include use of dewaxing catalysts based on an MEL framework structure (ZSM-11) to provide improved dewaxing activity. In some aspects improved dewaxing is achieved operating at lower pressures and with higher amounts of organic nitrogen slip from hydrotreatment.

公开(公告)号：EP3225678A2

公开(公告)日：2017-10-04

申请号：EP17151967.1

申请日：2005-03-08

申请人： China Petroleum & Chemical Corporation ,  Research Institute Of Petroleum Processing, Sinopec

发明人： Long, Jun ,  Da, Zhijian ,  Li, Dadong ,  Wang, Xieqing ,  Shu, Xingtian ,  Zhang, Jiushun ,  Nie, Hong ,  Xie, Chaogang ,  Zhang, Zhigang ,  Wang, Wei

IPC分类号： C10G11/18 ,  C07C4/06

CPC分类号： C10G69/04 ,  C07C4/06 ,  C07C5/05 ,  C07C5/11 ,  C10G11/18 ,  C10G69/02 ,  C10G69/06 ,  C10G69/14 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2300/4093 ,  C10G2300/44 ,  C10G2300/807 ,  C10G2400/20 ,  C10G2400/30

摘要： A process for producing light olefins and aromatics, which comprises reacting a feedstock by contacting with a catalytic cracking catalyst in at least two reaction zones, wherein the reaction temperature of at least one reaction zone among the reaction zones downstream of the first reaction zone is higher than that of the first reaction zone and its weight hourly space velocity is lower than that of the first reaction zone, separating the spent catalyst from the reaction product vapor, regenerating the separated spent catalyst and returning the regenerated catalyst to the reactor, and separating the reaction product vapor to obtain the desired products, light olefins and aromatics. This process produces maximum light olefins such as propylene, ethylene, etc from heavy feedstocks, wherein the yield of propylene exceeds 20% by weight, and produces aromatics such as toluene, xylene, etc at the same time.

摘要翻译： 一种生产轻质烯烃和芳族化合物的方法，该方法包括在至少两个反应区中通过与催化裂化催化剂接触使原料反应，其中第一反应区下游反应区中至少一个反应区的反应温度高于 与第一反应区相比，其重时空速低于第一反应区，将废催化剂与反应产物蒸气分离，再生分离的废催化剂并将再生的催化剂返回反应器， 反应产物蒸气以获得所需产物，轻质烯烃和芳族化合物。 该方法从重质原料中产生最大量的轻质烯烃如丙烯，乙烯等，其中丙烯的产率超过20重量％，并同时产生芳族化合物如甲苯，二甲苯等。

公开(公告)号：EP3221429A1

公开(公告)日：2017-09-27

申请号：EP15797556.6

申请日：2015-11-10

申请人： Exxonmobil Research And Engineering Company

发明人： XU, Xiaochun ,  WILSON, Keith ,  SOLED, Stuart, Leon ,  MISEO, Sabato ,  LEVIN, Doron ,  BAUMGARTNER, Joseph, Ernest

IPC分类号： C10G45/08 ,  C10G45/50 ,  C10G65/04 ,  C10G65/08

CPC分类号： C10G45/50 ,  B01J23/882 ,  B01J23/883 ,  B01J23/888 ,  B01J23/8885 ,  B01J37/20 ,  C10G35/06 ,  C10G45/08 ,  C10G47/06 ,  C10G65/02 ,  C10G65/04 ,  C10G65/08 ,  C10G65/12 ,  C10G67/04 ,  C10G69/02 ,  C10G69/08 ,  C10G2300/1048 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2400/00 ,  C10M101/02

摘要： Methods are provided for hydroprocessing a feed (such as hydrotreating, hydrocracking, or hydrofining a feed) to generate a product with a reduced or minimized aromatics content relative to the severity of the hydroprocessing conditions. In some types of hydroprocessing applications, it can be desirable to select the severity of hydroprocessing conditions to achieve a desired level of removal for sulfur, a desired level for removal of nitrogen, and/or a desired level for increasing the viscosity index of a feed. The severity for heteroatom removal and/or viscosity index uplift can also correspond to an amount of conversion of a feed to lower boiling point products, so the lowest severity conditions suitable for achieving a product quality can be desirable. By improving the aromatics saturation during hydroprocessing, the severity of subsequent aromatics saturation processes can be reduced.

公开(公告)号：EP3201296A1

公开(公告)日：2017-08-09

申请号：EP15781261.1

申请日：2015-10-01

申请人： Saudi Arabian Oil Company

发明人： ABUDAWOUD, Raed ,  AL-AMER, Mohammed

IPC分类号： C10G69/08 ,  C10G69/10 ,  C10G59/02 ,  C10G63/02

CPC分类号： C10G69/02 ,  C10G59/02 ,  C10G63/02 ,  C10G69/08 ,  C10G69/10 ,  C10G2400/30

摘要： The present invention relates to methods and systems useful for producing aromatics-rich products from liquid hydrocarbon condensates. The production system includes a hydroprocessing reactor, an aromatization reactor system and a hydrogen extraction unit. The methods for producing the aromatics-rich products include introducing a wide boiling range condensate into the hydroprocessing reactor and operating the aromatics production system such that the hydroprocessing reactor forms a naphtha boiling temperature range liquid product. The liquid hydrocarbons produced in accordance with the present invention may optionally be further processed using a hydrogen extraction unit to produce a high-purity hydrogen fraction.

摘要翻译： 本发明涉及可用于从液态烃冷凝物生产富含芳烃的产物的方法和系统。 该生产系统包括加氢处理反应器，芳构化反应器系统和氢提取单元。 生产富含芳烃的产物的方法包括将宽沸程冷凝物引入加氢处理反应器并操作芳烃生产系统，使得加氢处理反应器形成石脑油沸点温度范围的液体产物。 根据本发明产生的液态烃可以任选地使用氢提取单元进一步处理以产生高纯度氢馏分。

公开(公告)号：EP3201295A1

公开(公告)日：2017-08-09

申请号：EP15781260.3

申请日：2015-10-01

申请人： Saudi Arabian Oil Company

发明人： ABUDAWOUD, Raed

IPC分类号： C10G69/08 ,  C10G69/10 ,  C10G59/02 ,  C10G63/02

CPC分类号： C10G69/02 ,  C10G59/02 ,  C10G63/02 ,  C10G69/08 ,  C10G69/10 ,  C10G2400/30

摘要： The aromatics production system is useful for producing an aromatics-rich system product from a liquid hydrocarbon condensate includes a hydroprocessing reactor, an aromatization reactor system and a hydrogen extraction unit. The method for producing the aromatics-rich system product from the wide boiling range condensate includes introducing the wide boiling range condensate into the hydroprocessing reactor, operating the aromatics production system such that the hydroprocessing reactor forms a naphtha boiling temperature range liquid product, such that the aromatization reactor system forms the aromatics-rich system product, and such that the hydrogen extraction unit forms a high-purity hydrogen.

摘要翻译： 芳烃生产系统用于由液态烃冷凝物生产富含芳烃的系统产物，包括加氢处理反应器，芳构化反应器系统和氢提取单元。 由宽沸程冷凝液生产富含芳烃的体系产品的方法包括将宽沸程冷凝液引入加氢处理反应器，操作芳烃生产体系，使得水力沸腾反应器形成石脑油沸点温度范围的液体产品，使得 芳构化反应器系统形成富芳烃体系产物，并且使得氢提取单元形成高纯度氢。

公开(公告)号：EP3170802A1

公开(公告)日：2017-05-24

申请号：EP16203619.8

申请日：2010-10-11

申请人： Elevance Renewable Sciences, Inc.

发明人： COHEN, Steven A. ,  LUETKENS, Melvin L. ,  BALAKRISHNAN, Chander ,  SNYDER, Robert

IPC分类号： C07C6/02 ,  C10G50/00 ,  C10L1/08 ,  C07C51/09 ,  C07C67/03 ,  C07C67/333 ,  C07C69/533 ,  C10G45/00 ,  C10G45/58 ,  C10G65/04 ,  C11B3/00 ,  C10L1/02 ,  C11C3/00 ,  C10G3/00 ,  C07C6/04 ,  C10G69/02 ,  C10L1/04

CPC分类号： C10G3/42 ,  C07C2/862 ,  C07C6/04 ,  C07C51/09 ,  C07C67/03 ,  C07C67/54 ,  C07C2531/14 ,  C07C2531/24 ,  C10G45/00 ,  C10G45/58 ,  C10G50/00 ,  C10G65/043 ,  C10G69/02 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/30 ,  C10G2300/301 ,  C10G2300/307 ,  C10G2300/308 ,  C10G2300/44 ,  C10G2400/00 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/22 ,  C10L1/026 ,  C10L1/04 ,  C10L1/08 ,  C10L2200/0469 ,  C11B3/00 ,  C11C1/08 ,  C11C3/003 ,  Y02E50/13 ,  Y02P30/20 ,  Y02T50/678 ,  C07C69/533 ,  C07C57/03 ,  C07C57/12 ,  C07C11/02

摘要： Methods are provided for producing fuel compositions. The methods comprise reacting a feedstock in the presence of a metathesis catalyst under conditions sufficient to form a metathesized product comprising olefins and esters. The methods further comprise hydrogenating the metathesized product form a fuel composition.

摘要翻译： 提供了用于生产燃料组合物的方法。 该方法包括在足以形成复分解产物包含烯烃和酯的条件下反应在复分解催化剂的存在下的原料。 所述方法还包括氢化所述复分解产物形成的燃料组合物。

公开(公告)号：EP2609177B1

公开(公告)日：2017-03-08

申请号：EP11820525.1

申请日：2011-08-23

申请人： KiOR, Inc.

发明人： RAMIREZ-CORREDORES, Maria, Magdalena ,  SANCHEZ, Vicente

IPC分类号： C10G69/02 ,  C10L1/00 ,  C10L1/02 ,  C10B49/02 ,  C10B53/02 ,  C10C5/00 ,  C10G3/00

CPC分类号： C10B49/02 ,  C10B53/02 ,  C10C5/00 ,  C10G3/46 ,  C10G3/50 ,  C10G69/02 ,  C10G2300/1014 ,  C10G2300/202 ,  C10G2300/203 ,  C10G2300/301 ,  C10L1/023 ,  C10L1/026 ,  Y02E50/13 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/20

公开(公告)号：EP3102655A1

公开(公告)日：2016-12-14

申请号：EP15704977.6

申请日：2015-02-06

申请人： Linde AG

发明人： DELHOMME-NEUDECKER, Clara ,  HÖFEL, Torben ,  SCHÖDEL,Nicole ,  ZIMMERMANN, Heinz ,  HAIDEGGER, Ernst ,  KRACKER-SEMLER, Gunther ,  SCHMADERER, Harald

IPC分类号： C10G45/32 ,  C10G69/02 ,  C10G69/06 ,  C10G3/00 ,  C10G9/36 ,  C07C1/20 ,  C07C7/08 ,  C07C7/00

CPC分类号： C07C7/005 ,  B01D3/143 ,  C07C1/20 ,  C07C7/04 ,  C07C7/163 ,  C10G3/00 ,  C10G9/36 ,  C10G45/32 ,  C10G69/02 ,  C10G69/06 ,  C10G2400/20 ,  C10G2400/22 ,  Y02P30/20 ,  C07C11/02

摘要： A process (100) for obtaining olefins is proposed in which a first gas mixture (b), generated by a steam cracking process (1), is used at least partly to form a first separation feed (f) which comprises hydrocarbons having one to five carbon atoms, and from which at least a first separation product (g) and a second separation product (h, o) are produced, the first separation product (g) comprising at least the predominant fraction of the one- and two-carbon-atom hydrocarbons present in the first separation feed (f), and the second separation product (h, o) comprising at least the predominant fraction of the four- and five-carbon-atom hydrocarbons present in the first separation feed (f), and in which a second gas mixture (r), generated by an oxygenate-to-olefin process (2), is used at least partly to form a second separation feed (t) which comprises hydrocarbons having one to five carbon atoms, and from which at least a third separation product (e, y) and a fourth separation product (l, z) are produced, the third separation product (e, y) comprising at least the predominant fraction of the one- and two-carbon-atom hydrocarbons present in the second separation feed (t), and the fourth separation product (l, z) comprising at least the predominant fraction of the four- and five-carbon-atom hydrocarbons present in the second separation feed (t). The third separation product (e, y) is likewise used at least partly to form the first separation feed (f), and from at least part of the fourth (l, z) and second (h, o) separation products a third separation feed (h, l)(o, z) is formed and is subjected to a separation (14).

摘要翻译： 提出了一种用于获得烯烃的方法（100），其中通过蒸汽裂解方法（1）产生的第一气体混合物（b）至少部分地用于形成含有烃的第一分离原料（f） 1至5个碳原子，并且从其中至少产生第一分离产物（g）和第二分离产物（h，o），第一分离产物（g）至少含有较大比例的烃与一个碳 原子和含有第一分离原料（f）中的两个碳原子的烃，和含有至少较大比例的具有四个碳原子的烃和具有五个碳原子的烃的第二分离产物（h，o） 包含在第一分离原料（f）中，并且其中使用由含氧化合物至烯烃方法（2）生产的第二气体混合物（r）至少部分地用于形成含有烃的第二分离原料（t） 与o 从而从其中产生至少第三分离产物（e，y）和第四分离产物（1，z），所述第三分离产物（e，y）至少含有较大比例的 含有一个碳原子的烃和在第二分离原料（t）中包含两个碳原子的烃，第四分离产物（1，z）至少含有比例大于4或5个碳原子的烃 第二分离原料（t）。 第三分离产物（e，y）还至少部分地用于形成第一分离原料（f），并且第三分离原料（h，l）（o，z）由第四分离的至少一部分形成 产物（l，z）和第二分离产物（h，o）并进行分离（14）。

公开(公告)号：EP2737019A2

公开(公告)日：2014-06-04

申请号：EP12819035.2

申请日：2012-07-27

申请人： Saudi Arabian Oil Company

发明人： KOSEOGLU, Omer, Refa

IPC分类号： C10G25/00 ,  C10G67/06 ,  C10G65/16 ,  C10G65/00 ,  C10G65/04 ,  C10G67/00 ,  C10G67/16 ,  C10G45/58

CPC分类号： C10G69/02 ,  B01J19/245 ,  B01J2219/24 ,  C10G25/00 ,  C10G45/58 ,  C10G65/00 ,  C10G65/043 ,  C10G65/16 ,  C10G67/00 ,  C10G67/06 ,  C10G67/16 ,  C10G2300/1059 ,  C10G2300/1096 ,  C10G2300/202 ,  C10G2300/301 ,  C10G2300/44

摘要： Deep desulfurization of hydrocarbon feeds containing undesired organosulfur compounds to produce a hydrocarbon product having low levels of sulfur, i.e., 15 ppmw or less of sulfur, is achieved by first subjecting the entire feed to an extraction zone to separate an aromatic-rich fraction containing a substantial amount of the aromatic refractory and sterically hindered sulfur-containing compounds and an aromatic-lean fraction containing a substantial amount of the labile sulfur-containing compounds. The aromatic-rich fraction is contacted with isomerization catalyst, and the isomerized aromatic-rich fraction and the aromatic-lean fraction are combined and contacted with a hydrotreating catalyst in a hydrodesulfurization reaction zone operating under mild conditions to reduce the quantity of organosulfur compounds to an ultra-low level.

摘要翻译： 通过首先将整个进料进料到提取区以分离富含芳族化合物的馏分，从而实现含有不需要的有机硫化合物的烃进料的深度脱硫以产生具有低含量硫的烃产物，即15ppmw或更少的硫。 大量的芳族耐火和空间位阻含硫化合物和含有大量不稳定含硫化合物的芳族贫乏馏分。 将富含芳烃的级分与异构化催化剂接触，并将异构化的富含芳烃的馏分和贫芳族馏分合并，并在温和条件下加氢脱硫反应区中与加氢处理催化剂接触，以将有机硫化合物的量减少至 超低水平。